Catalytic oxidation of anthracene



Patented Dec. 30, 1930 UNITED STATES fP E meme

ALPHONS O. JAEGER, OF GRAFTON, PENNSYLVANIA, ASSIGNOR TO THE SEL'DEN'COM- PANY, OF PITTSBURGH, PENNSYLVANIA, A CORPORATION OF DELAWARE V V CATALYTIC OXIDATION OF ANTHRACENE No Drawing. Original application filed AugustS, 1927, Serial naainsas. minded and this application filed March 29, 192 8.

This invention relates to the catalytic oxi dation of anthracene to anthraquinone in'the vapor phase; I p 7 According to the present invention anthraceneis oxidized to anthraquinone in the vapor phaseby means ofair or other oxidizing ga s, in the presence of a new class of catalysts or contact masses, namely, catalysts or contact masses which contain non-silicious base exchange bodies, diluted or undiluted. Some of these new catalysts and contact masses have been described and claimed as products in my Patent No. 1,694,620, dated December 11, 1928, of which the presentapplication isin part a continuation. The catalytic oxidation of organic compounds generally by means of catalysts or contact masses containing non-silicious base exchange bodies has been described and claimed broadlyin my application Serial No. 211,638, filed August 8, 1927, which matured into Patent No. 1,735,763,dated November 12, 1929, of which the present application is a division.

The non-silicious base exchange bodies used in the present invention may be produ ced by the reactionlof metallate components with metal salt components under conditions so that the reaction mixture remains substantially alkaline to litmus. The invention is in no sense restricted to the use of catalysts which are the reaction products of a single 'metallate and a single metal salt component, and some of the most effective catalysts for use in the present invention are the reaction products. of a plurality of metallate components with one or more metal salt components or a plurality of metal salt components with one or more metallate components; t

Allof'the base exchange bodies used in the present invention, that is to say catalytically active bodies which are prepared by the reaction of a single inetallate with a single metal salt or bodies produced by'the reaction of at least one metallate with a plurality of 'metal salts, or vice vers a, possess a remarkably porous, frequently microporous, structure and in some cases are opalescent, When suitable catalytically active components are present in the products, they form catalysts Serial No. 265,819.

of remarkable eficiency due probably to the complexity, and the exact chemicalconstitutionjhas not been determined. In fact it is not even definitely determined whether single chemical compounds are formed in any or all. casesand it is possible that molecular mixtures are present; The products possess a physically microscopical homogeneity and behave in manyways as if they were single compounds, and I am of the opinion'that probably in many cases the products are in factsingle compounds of very high molecular weight, but the invention is not limited to any theories of the chemical constitution of theproducts.

' It should be'clearly' understoodthat the products used inthepresent invention are chemically quite distinct from base exchanging bodies containing silicon,- such as for ex- It is of course possible that the cat- The molecular complexes which aiepresent are apparently of great size and ample the zeolites and related base exchange bodies and theiroeri vatives. The present compounds contain no silicon in their structure, and wvhile they share many of the physical properties of zeolites, namely, the a highly porous structure and-the power of exchanging their alkali cations for other cations by base exchange, they are chemically distinct products. Surprising as it may seem, the presence of silicon, which has hith 1 erto been considered as essential tothe for- -mation of the skeletons of such advantageous physical structure, appears to be only one of many elements which are capable of bringing about these physical properties and many of the base exchange bodies of the pres ent invention possess all of the mechanical strength and'resistance of the silicious zeolit-es, properties whichare of course of utturewhich is substantially neutral or alka- .line to phenolphthalein, products having'a higher states of oxidation, and can begused;

singly or in mixtures as the metallate components for producing base exchangebodies" used inithe present inventiomit .beingnnder stood ofcoursethat the choice will depend on the metal saltsto be used and on the catalytic effects which it is desired to produce; Among the elements which form metallates are the" following :'alumm'um, chromium,-

Zinc, vanadium, beryllium, tin, palladium, platinum, titanium, zirconium, tungsten, uranium, tantalum, boron and molybdenum. The elements which form the metallates may be present in the forum-of their oxidesor hydroxides united withalkali to form simple metallates, or they may "be present partly or wholly in the form of complex compounds, such as for example, ammonia complexes, cyanogen complexes, and the like. In general, the complex compounds described in the copending application of 'Jaeger and Bertsch, Serial No. 100,116, filed April 6 1926, may be used. 7 y

The metal alt components include the water soluble, neutral or acid salts of the following elements :-copper, silver, gold, beryllium, 'zinc, cadmium, aluminum, rare earths, titanium, zirconium, tin, lead, thorium, chromium, uranium, vanadium, manganese, iron, nickel, cobalt, platinum, pal-- ladium, which may be used alone or in any desired mixture. It is an advantage of the present invention that definite proportions of the individual compounds do not :need to be used, either because mixturesof different compounds are formed, ormore vprobably becausethe tremendous size and complexityof the moleculemasks any requirements for; definite proportions. V r

All of the products used in .the present invention possess base exchanging powers to a greater or less extent when first prepared in solutionswhich are substantially neutral or alkaline to phenolphthal'ein. For the oxidation of anthracene, however high base exchanging power of the products is not required and it is therefore possible to depart considerably from the optimum conditionsof production as far as base exchange power. goes. In other-wordathe limits ofalkalinity, neutrality or acidity are much Wider than in the caseof products which are to ing power. While usually the-highest baseexchanging powers are obtained whenthe compounds are produced in a reaction mixsimilar. physical structure and being desirable" for the catalytic oxidation of organic compounds can be prepared with somewhat 'cliiierent proportions of the components, so

that at the end of the reaction the mixture may possess any alkalinity or acidity between phenolphthaleinred and'liztiniis blue as indicator end points. J

" V The possibilities of producing catalysts according to the. presentinvention are not limited to the reaction products of the metallates and metal salt components which may be used and which are present in the molecules in a non-exchangeable form. On the contrary, a'further series of products can be prepared by exchanging part or all of the alkali cations forcother atoms or radicalshy means of base exchange. The number of cations which can be introduced is very large, and some of them are included in the following elements and r'adicals :am1nonium,

copper, silver, gold, beryllium, magnesium, 1

caesium, zinc, strontium, cadmium, barium, mercury, aluminum, thallium, tltanlum, zirconium, tln, thorium, vanadium, chromium,

u ranii'im, manganese,'iron, cobalt, nickel, palladium, platinum. These cations may be introduced either singly or in mixtures, simultaneously or successively. The wide possibilities of combination which can be efiected by theintroduc'tion of various cations by means of base exchange gives the catalytic chemist an almost infinite field of choice in preparing catalysts having just the right degree of activity 'fororga'nic oxidations and it is an advantage of the present invention that catalysts of'exceedijngly finely adjusted activity can be producedand are effective.

The cations introduced bybase exchange may be themselves catalytically actiy'e, or they may activate catalytic components which are present in the products in nonexchangeable form, Cations may also be introduced as simple ions 'or as complex ions. In all cases,

"'tlie'catal'y'tic activity of the products obtained is'enhanced by the favorable tur'e of the products.

physical struc- A further series of products can'be obtained by treating the base exchange bodies used in the present invention, either with or without the presence ofcations introduced by base exchange, with products containing anions which are capable of reacting with the base exchange body to form salt-like products. p

- In the contact masses containing salt-like bodies which are used in the present invention', "the catalytically efi'ectiv'e components be used for water softening, and which therebody, solely in the anion of the salt-like body,

may be present solely in the base exchange or partly'in one and partly in the other. Acid radicals of the following elements, either i -i i s or com e anions, smleacds, olacd plx canjbe usedin producing salt-like bodies with chromium, molybdenum, manganese, 'tanta-' ion lum, I arsenic, phosphorus, bismuth, sulfur, chlorine; platinum, boron. Complex ions, such as for example,"ferroand ferricyanogen,'sulfocyanogen, metal cyanogen, and the like,-may also be used wherever they form salt-like bodies with the baseexchange bodies of-th'epresent invention. A sin'gle acid radical may be introduced, or a mixture maybe used, eithe'r by a simultaneous or successive treatment. The amount of the acid radical used may also be variedso that the products I may possess the character of acid, neutral or basic salts. I

While it is possible to use certain of the catalysts of the present invention in an undiluted form, best results are usually obtained by the dilution of the products with more or less inert bodies, or with bodies of relatively feeble catalytic powers or activating powers. Diluents can be incorporated with the cataly'ti'cally active base exchange body before or after formation, and are preferably although not necessarily, incorporated therewith to produce a physically homogeneous structure. In addition to finely divided carriers,

diluted or undiluted catalytically active base v and particularly after drying, it is of course impossible/to incorporate diluents into the base exchange body other than by purely physical mixture, which in generalis less desirable, but which is not-excluded from the t broader aspects of the present invention.

A; large number of diluent bodies can be used, such as silicious materials, as kieselguhrs of all kinds, diatomite brick refuse, 'pumicemeal, pulverized quartz, sand, and 'othermi'nerals, especially. those rich in silica. In the same way, a large number of natural or artificialmassive carrier fragments can be 'used,--sucl1 as fragments .of pumice, diatomite bricks or other minerals, metal, granules and the like. In general,. the methods of incorp'o'ration and many of the diluents which can "'beuse'd are described in the co-pending ap- -pli.cati'on of Jaeger and Bertsch, Serial No. 95,771, filed March 18, 1926. v v j The high porosity of tlie.products which are prepared may beeven further increased by incorporating into the framework of the lnuae exchange body products which can be -i :emoved -by leaching, "volatilization or; oom- "bustien, and which-when removed leave adniany cases are of importance.

the metall'ates,.the amphoteric metals may ditional porous spaces and, produce an even more advantageous physical structure. The substances added may be of organic or inorganic nature and may be added as individuals or may be in chemical combination with some of the permanent components. Thus, for example, certain of the components may be introduced in the form of complex compounds which are later decomposed and then leave additional porous spaces. Examples of such compounds are certain ammonia complexes which can be decomposed by heating the finished product.

In general, the reaction of the component solutions results, in the production of soluble salts which are not wanted,and it is therefore usually desirable to wash the base exchange body, after precipitation, and. then to dry,

or dry first and then wash. I have found that while it is possible in some cases to dry at high temperature, forthe'best resul sin most cases drying temperatures of 100 C.,

or less,.are desirable.

In the general methods described above, separately prepared metallate components and metal salt components havebeen caused to react. lVhile for many purposes these are the preferred methods, it is-possible to prepare base exchange bodies by somewhat different methods. Thus, for example, if a solution of a metallate of amphoteric metal is. cautiously neutralized with acid until the stronglyalkaline reaction becomes Weakly alkaline to phenolphthalei'n, or even slightly acid with weak alkalinity to litmus as a limit, base exchange bodies are produced, and in Instead of also be present in the form of complex metallate co n'ipounds,for example, such complex compounds asare describedin the copending application of Jaeger and Bertsch, referred to above. v

In a similar manner, acid or neutral solutions of saltsnof amphoteric metals may be treated with alkali until the mixture becomes neutral or alkaline to phenolphthalein, or even acid, in which'case base exchange bodies are produced in a manner similar to that de scribed inthe foregoing paragraph. The base exchange bodies produced either by neutralizing metallate solutions or metal salt solutions in general. do not show quite'as great base exchange, power as do those which are prepared by causing ready made metallate and .metal salt solutions to react with each other. The physical structure, however, appears to besimilar and, as in manycases. particularly in the oxidation of anthracene. extremely high base exchange power is not essential. Many very valuable catalysts can be produced in this manner. I p I A further wet preparation consists in causing alkalimetal salts of the oxygen-containing acids of metal elements of the fifth and sixth groups of the periodic system,such, as

for example, vanadium, molybdenum, tantaother metallates. V

In addition to the Wet methods, which for most purposes Iiind are preferable, base exchange bodies can be produced by fusion methods, for example, by fusing'oxides o1 hydroxides of the metallate and metal salt 'componentswith alkali,such as, sodium carbonate of potassium carbonate ortheir hydroxides The base exchange bodies produced by fusion, While sometimes they do not possess quite as high base exchange powers, are nevertheless of a similar advantageous physical structure, and many or" the products are yery valuable catalysts. v Oxides of the metals of the fifth and sixth groups may also be used to form products somewhat similar to those described in the preceding paragraph base exchange body itself, and many very important catalysts can be produced in Which catalyti'cally'inactive base exchange bodies are united'with catalytically active diluents to' form physically homogeneous r-masses. These masses, although they do not contain catalytic elements chemically combinedwith the base exchange body, of course share its microporous structure, and Where suitable catalytically active diluents are used,catalysts of greatefliciency are obtained, and are included in the scope of the present invention. Of course the catalytic activity may 'reside both in the diluents and in thebase exchange The catalysts usedin the present invention, and particularly ,diluted catalysts, may in many cases with advantage be given a preliminary treatment consisting in a calcinetion' and exposure to oxldizing or acid vapors at an elevated temperature as described-in my Patents 1,678,626.a11d"l,678,627, dated July 24, 1928, Such treatments frequently produce secondary chemical changes as are produced in the catalysisthemselves, andit should be understood that the catalysts ofthe present invention are defined asto chemical composition as of the time when 1 they arefreshly made, in accordance :With the usual methods of definition catalytic chemmy; f i V 'tion of the impurities.

ma am Many of the organiereactions whichere included in the epresentinvention, and particularly the oxidation voft vanthracene, require a slowing down, or stabilizing, of the catalysts used, in ordertoiprevent excessive. losses through, total Combustion, or to permit stopping I at a definite intermediate oxidation product with maximumyield, I have found that the presence ofselts of alkali-jorming metals and other non-catalytic components may act as stabilizers, as may the oxides or hydroxides themselves in some reactions. Other catalytically active or activating substances which are :not. pecific catalysts for the oxidation of anthraeene to a h q i which enhance .the-efijecti e e the Stabilizers, and which are termed stabili P motors, may also be used. In, fa t Wllellwer base exchange catalysts of the pr n n ention which containexchangeable alkali met cations areigiven preliminary treatment with acid .vapors, alkali forming metal compounds areproduced which act as stabilizers, and

many of the amphoteric or other metal components which are not selective catalysts for the particular oxidation. reaction may be considered, and act as stabilizer promoters.

Ixlonotclain1 inthisiapplieation the use of stabilizers or stabilizer promoters in gen- .eral, as these form the subject-matter of my co-pending application, Serial No. 264,571,

filed Malt-24,1928. The expressions stabilizers:and"stabilizer promoters when used in the present application, are to be understood as used'in the'senseniniwhichthey are defined in the ,afore mentioned co-pending application.- It should be understood hat While many'of" the base exchange catalysts used in the present invention may be considered as composite stabilizers and stabilizer promoters, the invention is not limited thereto, and stabilizers or stabilizer promoters, or both, may be separatelyadded tothe oatalysts ofthe present invention, and in fact many of the diluents, for example those containing certain heavy or amphoteric metal compounds, are-to-be considered as stabilizer promoters.

a he present'invention is not only applicable to the oxidation of relatively pure or high gradeanthracene, but may also be used for the oxidation ofzimpure anthracene, for

, example, .anthracen'econtainin carbazole or phe-nanthreneas impurities. hen impure anthracene is oxidized the contact mass preferably should contain stabilizers or stabilizerpromoters which favor the total. combus- Thus for example strongly alkalinestabiIiZeI's, which are relatively poor stabilizers for'the oxidation of pure anthracene to .anthraquinone, are effective in the selective total combustion of carbazole and similar nitrogenous heterocyclic compounds. When impure anthracene is oxidized-the reaction may take I of Celite earth is added as a diluent.

second half of the original solution is then place in a single step, or it may take place in two steps, part ofthe contact mass favoring the selective combustion of impurities and part favoring the, oxidation of anthracene to anthraquinone. It is one of the great advantagesof the present invention that the'range of quality of anthracerie which can be used is very great, and relatively low grade anthracene' can be effecti\-'ely'handled. It should be understood that when the reaction takes place in asingle stage a compromise contact mass must be used as the most effective contact masses for the oxidation ofanthracene to anthraquinone are not always the most effective for the selective combustion of impurities. The best compromise will depend on the nature, of the crude anthracene used and on the nature of the contact mass chosen. r

The invention will be described in greater detail in connection with the following specific examples which are illustrative merely, anddo not limit the broader scope of the invention. The examples, however, do in 2. many cases contain specific features which in their more narrow aspects are included in the present invention. The-examples give a few typical reaction conditions and catalysts, but it should be understood that the skilled catalytic chemist will choose within the confines of the present invention catalysts and reaction conditions best suited to the particular installation in which he is interested.

E trample 1 ,vanadyl sulfate. The vanadyl sulfate solution is then divided into two parts, half of which is treated at -60 C. with sufiicient 5NKOH to form a clear coffee-brown solution of potassium vanadite, toswhich 50 pages added with vigorous agitation, care being taken that the alkalinity remains between phenolpthalein red and litmus blue. The

gelatinous product is sucked but not dried and constitutes a vanadyl base exchange body. i

10.2 parts of freshly precipitated aluminum oxide are brought into solution with 40 7 parts of 100% KOH in 200 parts of water.

The vanadyl base exchange body described above is then stirred into the solution and a ferric sulfate withj9 mols of water or 44.4

parts of aluminum sulfate with 18 mols of water or a mixture of the two is added to the aluminate mixture with vigorous agitation. The reaction product produced, whlch ls an of the/fifth and sixth groups, preferable with a1 1% ammonium'vanadate solution, resultin "a so-c'alledsal't-like body after the soluble components. have been washed out. The products are calcinedfwith air or gases containing carbon dioxide at 400 C. the calcination temperature being permitted to'rise gradually" in "order p to prevent undesirable changes inthe structure of the base'exchange body/TAfter this preliminary calcinat-ion the product maybe. preferably treated with 3 5% urner gases at 450 G. and is then 'readyfor use. f f I The contact mass so obtained is well suited for the' 'catalytic oxidation of 'anthracene to anthraquinone. The vapors of the anthracenemixed with air or other oxygen contain- .ing gases, such as, forexample, CO and oxygen, in the proportion of from 1,520 to l-r'30 are passed over the ,catalyst at 350- 420C. r j

' In this example the aluminum iron base exchange body may be considered as a complex stabilizer for the catalyst. In order to promote or tune the stabilizing actionof the catalyst various stabilizer promoters can be addedin the form of silicates or heavy metal ox des such as ferrlc oxide, copperoxide, t1- tanium diox de, manganese diox de, ZlICO- nium dioxide, cerium dioxide,beryllium ox- V ide, calcium oxide,coba-lt oxide or thorium dioxide: They may be added singly or in mixtures and mayadvantageously be formed in, a nascent state. Theamount of the stabilizer promoter added depends on the effect desired; in general from 245% of such stabi- "liz'er promoters gives good-results. These 'stabilizerpromoters, of course, may be added inthesame'manner as 'any'other diluent as "has been generally described in the introductory portion of this application.

' A' different method of introducing the stabilizer promoters consists in replacing part or all of themetalsaltcomponentsof the base exchange body with corresponding amounts of beryllium sulfate, silver-nitrate, nickel sulfate, cadmium sulfate or'similar mineral acid salts ofthesebases.'-

In'many cases'it-isdesirable to neutralize luents instead ofthe one 'de'scribed.

' mmiin otassiii inmate solutionjislprej'afed by transforming '15 parts of v Q' intothe potassium 'metayanadate ,with :N/QKOH then diluting" with 400 parts ofwaterq IO pa rts' MH'O and 50 parts o' i kiesei' ii-hr o anixture of c'an b'e used.

pumice meal are then stirred in. o these mixturesare added either lQl parts of freshly precipitated alumi m'm'oxide or '5. parts of aluminum oxiee and Rupert's-of freshl p cipitated ferric oxide, with sufficient NKOH solution to cause the entire mixture to r'eact neutral or weakly alkaline to .pheno lphthalei-n. T'he reaction mixture is then sucked and Worked ufpin the u'sual manner and aneflicient contact for the catalytic. oxidation of l V I air'rn the ratio of, 1:35 by welght and are passedfiover 't'he-contact'mass at 340 to 440 C.

anthracene to anthraquinone is obtained.

Ewdmple i? 1 2'parts of V O are suspendedini ZSO parts 7 of yvaterto.form a slurry, acidified with 5 parts of concentrated-sulfuric acid and then reduced to theblue yanadyl sulfate in the usualmanner for-example, by means 'ofgases =conta-ining Q which are passed into the solution at the boiling poil'it. 167 parts of aterg-lass solution at 33 B. are then diluted With 200 parts ofwater and about 60 parts'of Celite stirred in. The'waterglass solution is then-poured into the vanadyl sulfate solution With vigorous agitation, precipitating out yanadyl silicate; Care should be taken that-after all of-the solutions have reacted the resulting mixture must be nadef neutral to Litmus, if necessary with the help of small amounts of N.v sulfuric acid. 10 parts of freshly precipitated aluminum oxide are treated with suificient N/QKOH solution to dissolve upthe'aluminum oxide in the form of potassium aluminate and to priovide a 104% excess of I parts ofFe K Q;): 9 aq. are dissolved in 250 to300 parts of Water. v

Instead'of using this latter salt component for'the formation of the base exchange'body, correspondin amounts of titanium sulfate, aluminum su fate, copper nitrat e, cobalt nitrate, nickel sulfate, thoriumf-nitratef silver nitrate,-zirconiuin nitrate,&cerium-nitrate, or a he yanad-yl s -icate fis then stirredinto the -aluminatefsolution-diluted with Celite and thereupon the above mentioned salt compo- ;nent oncomponents are added producing a base exchange body in W hichthe vanady lsilicam is homogeneously incorporatedasa di- The reaction product is treated the usual be replaced by'i'ron, using a 5% iron sulfate so'lntion. Replacing the alkali of the base exchange by copper, silver, nickel and lead,

7 using a 5% to'lO solution of the-corresponding salts'o'r their mixtures, favorably influe'nc'e's the'catalyti'c e'flici'ency of such contact masses for the catalytic oxidation of organic compounds. 7

Treatme t with ammonium vanadate or lnolyb'date for the formation of the so-called salt li'ke body helps toenhance the catalytic efficiency for specific oxidation reactions and also the resistance of such contact masses against high temperatures often obtaining in these processes. I

Contact masses containing such com-ponents a're- Well suited for the catalytic oxidation of anthracene to anthraquinone.

' These organiccomp'ounds are mixed with y Ewample 4.

'QO 'ai-tsof 33 Be; sodium waterglass solution are'diluted with 1510 20 volumes of water and *60 80 parts of infusoria'l earth are added. Sufii'cien't 5% iron sulfate, copper sulfate, silver nitrate, calcium chloride, strontium chloride, and manganese nitrate solution, singly or in admixture, are added with vigorous agitation to bring about a neutral reaction to litmus. The precipitate is sucked "and thoroughly washed with water to get'thealka'li metal salt-out of it and then constitutes diluted neutral silicates of the metals used w'hich can'be further worked up without drying;

' 10 parts of A freshly precipitated, are transformed into potassium aluminate using a suiiicient amount of QINJKOH: solution to provide-an excess alkali amouiiting to about 10'% to 15%. The diluted silicates described "alcove are kneaded into this solution.

50 parts-of A1 (-,SO 18HgO are dissolved in'about 200 part'sof water. The latter'solution isthen kneaded with-the alum'inate nii'xture and "after'addition of all the solution,

an alkaline or neutral reaction to phenolphtha lein should be obtained.

, The diluted reaction product so obtained is freed rroinanctherhqaorby ressin -fined at 't'einperatures' n'nder 100 C. and broken in pieces. The dried fragments are leached out by trickling water over them and then are treated with 215% van-myIsunate solu- 7 tion, chromium nitrate sdlutioi or uranyl nitrate solution or "a mixture of "them, in orderto exeh'ange, as far as possible, the alkali "for these raflicaIs. Thereafter the product is impregnated with a di1utep'otassium or ammonium vanadate solution in sorial earth. 3

order to form the so calledsalt-like body, that is, the'vanadate of; the vanadyl b ase ex change body diluted with silicates and infu- After drying and calcining, the contact mass so obtained is very eflicient forf t he catalytic oxidation of anthi'a cene to anthraqur none when the vapors of the antliracene, mixed with air in the'ratio of 1 :20 by weight, are passed over the catalyst at 340 to i20 C. The'silicates act in this contact mass as stabilizer promoters in; the reaction and at the same time render the contact mass highly resistant to high temperatures often obtain ing in such catalytic oxidationprocesses.

Instead of neutral silicates, 5% to1'0%- of TiO Fe l) or MnO, singly or in admixture, can be used, the amount depending on'the diluent.

'Such a contact mass containing 6-8% of ferric oxide is particularly effective for the oxidation of anthracene to anthraquinone at a temperature of 350-400 C. when a mixture of anthracene and air in a proportion of 1 a0 is passed over the'catalyst.

Similar catalysts can be obtained by impregnating the diluents with ferric sulfate, silver nitrate or copper nitrate.

In most of the examples the metal salt solution is added to the metallate solution, and this may be considered as the preferred method for producing non-silicious base exchange bodies used as contact masses in the present invention, but it should be understood that the invention is not limited to the use ofcontact masses or catalysts produced by this prelitmus, and preferably a neutrality of alka linity to phenolphthalein.

What is claimed as new is: 1. A method of oxidizing anthracene to anthraquinone, which comprises vaporizing anthracene and causing the vapors to react with an oxidizing gas in the presence of a catalytically active component of thecontact mass being chemically combinedinor with the non-silicious base exchange body/ 4. A method of oxidizing anthraceneto anthraquinone, which comprises vaporizinganthracen'e andcausing. the vapors to react with an oxidizing gas iii the presence of a contact mass containing at least one nonsilicious base exchange body, at lease one catalytically active component of the contact mass'be'ing chemically combinedin or with the non silicious base exchange body in non exchangeable form:" a

5. A method of oxidizing anthracene to anthr'aquinone, which comprises vaporizing anthracene and causing'the vapors to react with an oxidizing gas in the presence of contact mass containing at least one diluted non-silicious base exchange body, at least one catalytically effective componentof. the contact massbeing physically associated with the non-solicious base exchange body in the form of a diluent.

6. A method of oxidizing, anthracene to anthraquinone, which comprises vaporizing anthracene andcausingthe vapors to react with an 'oxidizing 'gas in the presence of 'a contact mass containing at least one how silicious base exchange body, the contact mass also'containing at least one compound'of an leo element falling within the group including 1' alkali metals; alkaline earth metals, and earth metals whoseoxide's are not reducible by hydrogen.

7. A method- 6f oxidizing ant-hracene to anthracene and causing the vapors to react withanoxidlzmg gas n the presence of a contactmass containing at leastfionenonalkali metals, alkaline eartlrme'ta ls, and'earth metals Whose oxidesare notreducible by hydrogen andfat least one solid catalyst, nonspecific to anthracene oxidation.

8. A method of oxidizing :anthracene. to anthraquinone, which comprises vaporizing anthracene and causing the vapors to react with an oxidizing gas in the presence of a con- 7 anthraquinone, which comprises vaporizing 3 'silicious base exchange body, the contact mass also contalning at least one compound of an element falling Within the group iincluding tact mass containing-at least "one fnon-'- 3 silicious'basecexchange bod", atleast one. com-, pound of an element fallingwithin the group including'alkali-metals, alkalineearth metals, and earth metals Whose-oxides are not redacible by hydrogen chemically combined. in the non-siliciousbase exchange body;

9. A method of oxidizingjanthracene tofanthraquinone, which comprises vaporizing anthraocne and causingthe vapors toreact with. an. oxidizing gas in 'the presence of a contact mass containing at least one nonsilicio-us base exchange body, at leastone compound of anelement falling withinthe group; including: alkalimetals, alkaline earth metals, and earth metals whoseoxides are not reducibleby hydrogen and: at least one solid 7 catalyst, non-specific to anthracene' oxidation chemically combined or witlrthe non-silicious basefiexchangebody, v I a v 10. A method of oxidizing anthracene to anthraquinone, which comprises vaporizing anthracena and causing the vapors-to react with an oxidizing gas in the presence of a contact masswith acid gases.

anthracene and causing the vapors to react with anoxidizing gas 'm the presence of a contact mass: containing at least one diluted non-silicious base exchange body, at-least part of the diluents containing iron vanadate.

16.. A method according to claim 6,.inwhich the stabilizer is potassium. v I

17 A method according to claim 6, in which the stabilizer is formedin situ by treating the a non-alkaline compound of contact mass. containing at least one non- V silicious base exchange body,,at least one compound of an-elementfallingwithin the group v A 7 including alkali metals, alkalineearthmetals, and earth metalswhose oxides are not reduciblecby hydrogen.- andat least onesolid catalyst, nonspecific to anthracene oxidation chemically combined in or with the non-silici- 011s base exchange body. in non-exchangeable form.

1L. A. method. of oxidizing anthracene vto anthraquinone, which comprises vaporizing anthracene and causing, the vapors to react with an oxidizing gas in the presence of: acoIrtact mass containing 'at-least onenon-silicious base exchange body,c the contact.massi contain- 7 ing an oxy-compound ofVana-dinm as at least one of its catalytically active components.

12. A. method of oxidizing antliracene to anthraquinone, which'comprises vaporizing anthracene. and causmgthe vaporsto react loo with an oxidizing gas: in the presence of a contact mass containing. at least one non- ,siliciousbase exchangevbody, in which chemically combined Vanadium is present.v

13. A method, of; oxidizing anthra'cene to anthraqninone, which comprises vaporizing anthracene and causing the vapors to react with an oxidizing gashin. thevp'resence of a contact mass containing at least one nonsilicious-base exchange body, the. contact mass coutaining iron as a non-specific catalyst.

14. A. method of oxidizing anthracene to ,anthraqnlnone, which comprises vaporizing anthracene. and causing the yaporsi to 're'act with an: oxidizing gas inthepresence of. a 7 contact mass containing. at least one diluted non-siliciousbase exchange body, at. least part ofathe diluents containing vanadium. compounds;

method of oxidizing anthracene; to i alltllraq uinone, whichgcomprises vaporizing 

